Process and catalyst for upgrading gasoline
Process and catalyst for upgrading gasoline comprising durene (1,2,4,5-tetramethylbenzene) and pseudodocumene, the process comprises hydroisomerization of durene (1,2,4,5-tetramethylbenzene) and pseudocumene (1,2,4-trimethylbenzene) contained in the gasoline in presence of a catalyst comprising a sulfided base metal supported on an acidic carrier, thereby converting durene (1,2,4,5-tetramethylbenzene) to isodurene (1,2,4,5-tetramethylbenzene) and prehnitene (1,2,3,4-tetramethylbenzene) and converting pseudocumene (1,2,4-trimethylbenzene) to mesitylene (1,3,5-trimethylbenzene).
1. A process for upgrading a synthetic gasoline comprising durene (1, 2, 4, 5-tetramethylbenzene) and pseudocumene (1, 2, 4-trimethylbenzene) derived from catalytic conversion of methanol or a methanol-dimethylether mixture, the process comprising hydroisomerization of durene and pseudocumene contained in the synthetic gasoline in presence of hydrogen, a catalyst comprising sulfided nickel supported on an acidic carrier, and a sulfur dopant to produce an upgraded synthetic gasoline, wherein durene (1, 2, 4, 5-tetramethylbenzene) is converted to isodurene (1, 2, 3, 5-tetramethylbenzene) and prehnitene (1, 2, 3, 4-tetramethylbenzene) and pseudocumene (1, 2, 4-trimethylbenzene) is converted to mesitylene (1, 3, 5-trimethylbenzene), said upgraded synthetic gasoline has a reduced durene and pseudocumene content and an increased combined isodurene and prehnitene content relative to said synthetic gasoline, and the upgraded synthetic gasoline has at least the same octane rating as the synthetic gasoline.
2. The process of claim 1 , wherein the catalyst has a nickel content of 0.5 to 20 wt %.
3. The process of claim 1 , wherein the acidic carrier comprises a zeolite.
4. The process of claim 3 , wherein the zeolite has a SiO 2 /Al 2 O 3 ratio in the range of 15 to 300.
5. The process of claim 3 , wherein the zeolite comprises ZSM-5.
6. The process of claim 1 , wherein the acidic carrier comprises alumina.
7. The process of claim 1 , wherein the catalyst is supported on a mixture of ZSM-5 and alumina.
8. The process of claim 7 , wherein the catalyst comprises 1-5 wt % nickel, and an acidic carrier comprising the ZSM-5 and alumina in a ratio between 50:50 and 70:30.
9. The process of claim 1 , further comprising a step of separating a light fraction from the synthetic gasoline and by-passing the light fraction around the hydroisomerization.
10. The process according to claim 1 , wherein hydroisomerization conditions include a temperature of between 250° and 400° C.
11. The process of claim 1 , wherein the synthetic gasoline includes more pseudocumene than durene.